Preparation of vanadium III oxidic compounds, and dehydrogenation of paraffins

ABSTRACT

Disclosed is making an inorganic crystalline vanadium III oxidic compound from a pentavalent vanadium compound, which process comprises (1) reducing a pentavalent vanadium oxidic compound to substantially the V III  state by heating at 100° C. or less an aqueous medium slurry or solution of said pentavalent compound containing a reducing agent selected from hydrazine and hydrocarbylhydrazine, (2) providing in said aqueous medium, either before, during or after said reducing step, other metal cations in solution in the ratio called for by the desired crystalline compound, (3) removing the liquid aqueous medium, and (4) calcining the resulting dry solid at a temperature in the range from 400° to 800° C. in an inert atmosphere. 
     Also disclosed is the vapor phase catalytic dehydrogenation of paraffins using certain spinels and perovskites as catalysts.

This invention relates to an improved method of making inorganic crystalline vanadium III oxidic compounds. These compounds are generically called vanadites.

In a more specific aspect the invention concerns an improved method of making V^(III) crystalline spinel compounds and crystalline perovskite compounds.

The usual method of preparation of vanadites and related compounds consists of preparing an intimate physical mixture of the appropriate oxides, including a low-valent vanadium oxide such as V₂ O₃, having the cations in the atomic ratios corresponding to that of the desired final composition, and heating this mixture to a temperature sufficiently high to cause the reaction of one solid with the other and the formation of a new phase. The oxide mixture is usually prepared by grinding, followed by pressing, pelletting, and firing at temperatures from about 700° to about 1200° C. The sequence of grinding, pressing, and firing has to be repeated several times in order to obtain a nearly homogeneous phase. Since both the lower vanadium oxides (e.g., V₂ O₃), and the resulting products are unstable to air oxidation at high temperatures, the firing step is usually done in a vacuum, in an inert gas, or in a reducing atmosphere (H₂ or CO) (see e.g., Rogers et al., J. Phys. Chem. Solids, 24, 347-60 [1963], or H. Oshima, J. Amer. Ceramic Soc., 63, 504-507 [1980]). The starting vanadium oxides themselves, such as V₂ O₃, are prepared by hydrogen reduction of V₂ O₅ at 650°-1000° C. It is thus evident that the prior art procedures for the synthesis of vanadites and the like are complicated, time- and energy-consuming, and require very high temperatures.

It is an object of the invention to provide an improved method to prepare crystalline vanadium III oxidic compounds.

It is an object of the present invention to prepare vanadium spinel compounds by an improved process.

It is an object of the present invention to prepare vanadium perovskite compounds by an improved process.

It is a further object of the invention to prepare vanadium spinels from 5-valent vanadium compounds without resorting to high temperatures to reduce the vanadium to a +3 valence.

It is a further object to provide a process for dehydrogenation of paraffins using the vanadium III oxidic compounds, such as the vanadium spinels, as catalysts.

Other objects, as well as features, aspects and advantages, of the invention will become apparent from a study of the specification.

The foregoing and other objects are realized by the present invention according to which there is provided a process for making an inorganic crystalline vanadium III oxidic compound from a pentavalent vanadium compound, which process comprises (1) reducing a pentavalent vanadium oxidic compound to substantially the V^(III) state by heating at 100° C. or less an aqueous medium slurry or solution of said pentavalent compound containing a reducing agent selected from hydrazine and a hydrocarbylhydrazine, (2) providing in said aqueous medium, either before, during or after said reducing step, other metal cations in solution in the ratio called for by the desired crystalline compound, (3) removing the liquid aqueous medium, and (4) calcining the resulting dry solid at a temperature in the range from 400° to 800° C. in an inert atmosphere. Usually calcining temperatures are no more than 700° C.

Hydrazine is the now preferred reducing agent, but monohydrocarbylhydrazines (such as monoalkyl or monoarylhydrazines) are also especially suitable reducing agents. The hydrocarbyl group usually has 1-10C atoms.

In a more specific aspect of the present invention there is provided a process for making a compound selected from a crystalline spinel of the formula

    A.sup.II V.sub.2-x.sup.III C.sub.x.sup.III O.sub.4         formula ( 1)

or a crystalline perovskite of the formula

    D.sup.III V.sub.1-y.sup.III C.sub.y.sup.III O.sub.3        formula ( 2)

from a pentavalent vanadium compound, where A is one or more of Mg, Zn, Mn, Fe, Co, Ni, Cu and Cd; D is one or more of Y, the rare earths and Bi; C is one or more of Al, Ga, Cr, Fe and Co, x is zero to <2, usually zero to 1.9, and y is zero to <1, usually zero to 0.9, which process comprises (1) reducing a pentavalent vanadium oxidic compound to substantially the V^(III) state by heating at 100° C. or less an aqueous medium slurry or solution of said pentavalent compound containing a reducing agent selected from hydrazine and a hydrocarbylhydrazine, (2) providing in said aqueous medium either before, during or after said reducing step, A^(II), D^(III) and C^(III) cations in solution in the ratio called for by the selected formula, (3) removing the liquid aqueous medium, and (4) calcining the resulting dry solid at a temperature in the range from 400° to 800° C. in an inert atmosphere. Usually calcining temperatures are no more than 700° C.

In the foregoing, the rare earths are as recognized in the art: namely, atomic numbers 57 to 71.

The cations other than vanadium are usually added according to step (2) of the present process as salts of acids forming easily thermally destructible, non-oxidizing anions. Organic salts, such as acetates are often preferred.

In a now preferred aspect of the invention for making spinels of formula (1) where y is zero, hydrazine (in an amount of 0.5-3 moles per atom of V^(V)), is mixed with an aqueous solution of the A^(II) salt of a carboxylic acid, particularly the A^(II) acetate. To facilitate solubility, an additional amount of an organic carboxylic acid, such as acetic acid can be added. To the dispersion thus obtained, a compound of pentavalent vanadium, particularly ammonium metavanadate, is added slowly, at from about 30° to about 100° C., with agitation, as either a solid or an aqueous solution. After addition, the mixture is further stirred and heated, then evaporated and dried, preferably in an inert atmosphere, e.g., N₂. The dried material is then heated under an inert gas (nitrogen, argon, etc.) at from about 400° to about 700° C., for a period from 5 to 25 hours.

In the synthesis of vanadium-containing spinels according to the method of this invention, the X-ray powder diffraction analysis reveals, quite unexpectedly, the formation of a spinel structure at these low calcination temperatures. Moreover, the repetitive grinding and heating of the prior art methods are totally unnecessary.

The present invention described here is clearly superior to the prior art methods, since it allows preparation of vanadium III compounds spinels via aqueous low temperature reduction of the vanadium ion, followed by a calcination heat treatment at unexpectedly low temperatures. The formation of the desired crystalline phases at such low temperatures is particularly unexpected and unique.

According to another aspect of the invention, the spinels and perovskites defined in formula (1) and formula (2), where (2-x) and (1-y) are each at least 0.1, have been found to catalyze the dehydrogenation of C₂ -C₄ paraffins to olefins, especially propane to propylene, at very high selectivities approaching 100 percent. The reaction can be effected at 450° to 700° C. at contact times of 0.2 to 40 seconds.

The following examples of the invention are illustrative and are not to be considered limiting. In the dehydrogenation examples, summarized in Table 1, the runs were effected in a fixed tubular bed of catalyst. In the spinel preparation examples, deoxygenated water was used to prepare the solutions and slurries, and the operations were carried out under nitrogen.

EXAMPLE 1

Crystalline MgV₂ O₄ spinel was made as follows:

To a solution of 22.55 g Mg(OAc)₂.4H₂ O in 150 ml water, there was added 10.85 g hydrazine hydrate (97%). After warming to 65° C. 24.6 g NH₄ VO₃ was added dry, in small portions, with vigorous agitation. The mixture became progressively darker. After stirring 1/2 hour at 65°-70° C., the mixture was evaporated under N₂ at 90° C. max. The thick viscious mass was dried over night in N₂ at 130°-140° C. The brown-black solid was then treated 2 h @ 350° C. and 3 h @ 420° C. under N₂ ; followed by 21 hours @ 700° C. in flowing argon (tube furnace). X-ray powder diffraction data showed that the product was a spinel.

Analysis: 53.0% V; 13.0% Mg; 34.0% O (by difference); Calculated formula: Mg₁.03 V₂ O₄.09.

EXAMPLE 2

Crystalline ZnV₂ O₄ spinel was made as follows:

To a solution of 23.08 g of Zinc acetate dihydrate in 150 ml of water was added 10.52 g of hydrazine monohydrate dropwise. A voluminous precipitate of Zn(OH)₂ was obtained. Another 150 ml of water was added with stirring. To the stirred slurry was slowly added 24.61 g of NH₄ VO₃ (solid) at 65°-70° C. The mixture darkened slowly and became medium brown. On further evaporation at 85°-90° C., the residue thickened and became black-brown. It was dried overnight at 115°-130° C. It was then heated under nitrogen for 0.5 h at 500° C., 0.5 h at 600° C. and 24 h at 700° C. X-ray powder diffraction analysis showed the spinel structure.

Analysis: 42.8% V: 27.4% Zn: 29.8% O (by difference); Calculated formula: ZnV₂ O₄.4.

In Examples 3-5, summarized in Table 1, the vapor phase catalytic dehydrogenation of propane was effected at 500° C. in the presence of an equal volume of N₂ diluent, using the contact times shown. In Examples 3 and 4 the catalyst was the magnesium-vanadium spinel of Example 1, and 9 parts by weight were diluted with 1 part by weight silica. In Example 5 the catalyst was the zinc-vanadium spinel of Example 2, undiluted.

                  TABLE 1                                                          ______________________________________                                                           Contact  Propane  Selectivity                                Exam-             Time,    Conversion,                                                                             to Propene,                                ple No.                                                                              Catalyst    Seconds  Percent  Percent                                    ______________________________________                                         3     Mg/V spinel 12.5     7.4      94.9                                       4     Mg/V spinel 26       7.3      97.0                                       5     Zn/V spinel 10.6     4.8      100                                        ______________________________________                                    

EXAMPLE 6

Crystalline LaVO₃ perovskite is made as follows:

To a solution of 72.04 g of La(C₂ H₃ O₂)₃.1.5H₂ O in 500 ml of water is added 10.52 g of hydrazine monohydrate. After warming to 65° C., 24.6 g NH₄ VO₃ is added dry, in small portions, with vigorous agitation. After evaporation to near dryness, the solid mass is dried for 16 hours in N₂ at 130° C. The dried material is then heat treated under nitrogen for 2 hours at 350° C., 2 hours at 500° C. and 24 hours at 700° C.

EXAMPLE 7

Crystalline LaCr₀.5 V₀.5 O₃ perovskite is made as follows:

To a solution of 72.04 g of La(C₂ H₃ O₂)₃.1.5H₂ O in 500 ml of water is added 5.26 g of hydrazine monohydrate. After warming to 65° C., 12.31 g NH₄ VO₃ is added dry, in small portions, with vigorous agitation followed by 25.95 g Cr(C₂ H₃ O₂)₃.H₂ O. After evaporation to near dryness, the solid mass is dried for 16 hours in N₂ at 130° C. The dried material is then heat treated under nitrogen for 2 hours at 350° C., 2 hours at 500° C. and 24 hours at 700° C.

EXAMPLE 8

Crystalline ZnFeVO₄ spinel is made as follows:

To a solution of 23.08 g Zn(C₂ H₃ O₂)₂.2H₂ O in 300 ml of water is added 5.26 g of hydrazine monohydrate. After warming to 65° C., 12.31 g NH₄ VO₃ is added dry, in small portions, with vigorous agitation followed by 33.92 g Fe(C₃ H₅ O₃)₃, ferric lactate. After evaporation to near dryness, the solid mass is dried for 16 hours in N₂ at 130° C. The dried material is then heat treated under nitrogen for 2 hours at 350° C., 2 hours at 500° C. and 24 hours at 700° C.

As will be evident to those skilled in the art, various modifications of this invention can be made or followed in the light of the foregoing disclosure and discussion without departing from the spirit and scope of the disclosure or from the scope of the claims. 

We claim:
 1. A process for making a compound selected from a crystalline spinel of the formula

    A.sup.II V.sub.2-x.sup.III C.sub.x.sup.III O.sub.4         formula ( 1)

or a crystalline perovskite of the formula

    D.sup.III V.sub.1-y.sup.III C.sub.y.sup.III O.sub.3        formula ( 2)

from a pentavalent vanadium compound, where A is one or more of Mg, Zn, Mn, Fe, Co, Ni, Cu and Cd; D is one or more of Y, the rare earths and Bi; C is one or more of Al, Ga, Cr, Fe and Co, x is zero to <2, and y is zero to <1, which process comprises (1) reducing a pentavalent vanadium oxidic compound to substantially the V^(III) state by heating at 100° C. or less an aqueous medium slurry or solution of said pentavalent compound containing a reducing agent selected from hydrazine and a hydrocarbylhydrazine, (2) providing in said aqueous medium either before, during or after said reducing step, A^(II), D^(III) and C^(III) cations in solution in the ratio called for by the selected formula, (3) removing the liquid aqueous medium, and (4) calcining the resulting dry solid at a temperature in the range from 400° to 800° C. in an inert atmosphere.
 2. A process of claim 1 wherein step (1) contains hydrazine as a reducing agent. 